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US4213826A Expired / Lapsed US ⏱️ 0.0 years remaining

Fluidized coal carbonization

Assignee: Cogas Development Co
•
Filing: 1978-10-02
•
Granted: 1980-07-22
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Expires: 1998-10-02
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Abstract

Abstract In the multi-stage fluidized carbonization of coal to produce, oil, gas and char, oil containing vapors from the first stage are used as the fluidizing gas to dry the incoming coal feed. The oil vapor pressure of the fluidizing gas is maintained at a value under 10 mm. to prevent oil condensation in the fluidized drying vessel. The technique makes possible the recovery of sensible heat from the first stage overheads.

Inventors

  • 👤 Ralph T. Eddinger
  • 👤 Louis D. Friedman

Bibliographic Details

Application Number —
Jurisdiction US
Data Source google_patents
Last Synchronized 2026-11-06 12:08
CPC Classifications
C; C10; C10B; C10B49/00; C10B49/02; C10B49/04; C10B49/08; C10B49/10; Y; Y02; Y02P; Y02P20/00; Y02P20/10; Y02P20/129; Y10; Y10S; Y10S208/00; Y10S208/951

Claims Analysis

Total Claims: 4
Claim 1
Independent Claim 244 words
In the multistage fluidized carbonization of coal to produce oil, gas and char wherein the coal is: 1. Heated in a first stage below its fusion temperature under oxygen free conditions in a first fluidized bed formed by passing an inert gasiform stream upwardly through the stage to maintain the coal in the fluidized state; 2. In at least a second stage passing the so-treated coal into at least one other fluidized bed which is fluidized by the gaseous overheads from the subsequent stages at a temperature above that of the first bed and below the fusion point of the solids fed to that stage, under oxygen-free conditions, for a time sufficient to remove nearly all of the volatiles from the coal condensable oily liquids, and 3. In a final stage passing the thus-treated coal into a final fluidized bed which is fluidized by an oxygen-containing gas at a still higher temperature, to substantially devolatilize the coal, the improvement of recovering sensible heat from the overheads of stage 1 comprising the steps (1) providing a fluidized drying zone to receive the particulate coal feed; (2) using the stage 1 overheads as the fluidizing atmosphere in step (1) to heat and dry the particulate coal feed while maintaining the vapor pressure of the oil in the drying zone at a value of under 10 mm; (3) conveying the dried coal to stage 1; and (4) recovering oil from the overheads of the fluidized drying zone.
Claim 2
Dependent Claim 244 words
In the multistage fluidized carbonization of coal to produce oil, gas and char wherein the coal is: 1. Heated in a first stage below its fusion temperature under oxygen free conditions in a first fluidized bed formed by passing an inert gasiform stream upwardly through the stage to maintain the coal in the fluidized state; 2. In at least a second stage passing the so-treated coal into at least one other fluidized bed which is fluidized by the gaseous overheads from the subsequent stages at a temperature above that of the first bed and below the fusion point of the solids fed to that stage, under oxygen-free conditions, for a time sufficient to remove nearly all of the volatiles from the coal condensable oily liquids, and 3. In a final stage passing the thus-treated coal into a final fluidized bed which is fluidized by an oxygen-containing gas at a still higher temperature, to substantially devolatilize the coal, the improvement of recovering sensible heat from the overheads of stage 1 comprising the steps (1) providing a fluidized drying zone to receive the particulate coal feed; (2) using the stage 1 overheads as the fluidizing atmosphere in step (1) to heat and dry the particulate coal feed while maintaining the vapor pressure of the oil in the drying zone at a value of under 10 mm; (3) conveying the dried coal to stage 1; and (4) recovering oil from the overheads of the fluidized drying zone.
Claim 3
Dependent Claim 19 words
The method according to claim 1 wherein the oil vapor pressure of the oil is 4 to 6 mm.
Claim 4
Dependent Claim 22 words
The process according to claim 1 wherein the coal is dried at a temperature of about 300° F. to about 350° F.

References Cited (Backward Citations)

US2773018A Cited
US2955077A Cited
US3043752A Cited
US2955988A Cited
GB1006043A Cited
US3375175A Cited
US3573194A Cited
US3836435A Cited
US4056443A Cited

USPTO Annuity & Maintenance Windows

Annuity Stage Window Opens Payment Deadline Surcharge Period Until Estimated Fee Status
3.5 Years (Year 4) 1983-07-22 1984-01-21 1984-07-22 $2000.00 Window Closed / Lapsed
7.5 Years (Year 8) 1987-07-22 1988-01-21 1988-07-22 $3760.00 Window Closed / Lapsed
11.5 Years (Year 12) 1991-07-22 1992-01-21 1992-07-22 $7700.00 Window Closed / Lapsed

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